Process for deasphalting a hydrocarbon oil
    1.
    发明授权
    Process for deasphalting a hydrocarbon oil 失效
    烃油脱沥青的方法

    公开(公告)号:US4816140A

    公开(公告)日:1989-03-28

    申请号:US32699

    申请日:1987-04-01

    IPC分类号: C10G21/00 C10G31/11 C10L3/00

    CPC分类号: C10G21/003 C10G31/11

    摘要: For deasphalting an asphaltene-containing hydrocarbon oil, employed is a hydrocarbon solvent of 3-8 carbon atoms, resulting in an asphaltic phase and a solution of deasphalted oil in the solvent. The solvent is then separated from the deasphalted oil, by passing the solution tangentially across an inorganic membrane of pore radii from 2 to 15 nonometers: the obtained filtrate has an increased solvent content and may be recycled. The deasphalted oil is selectively retained on the upstream side of the membrane.

    摘要翻译: 对于含沥青质的烃油进行脱沥青,使用的是3-8个碳原子的烃溶剂,导致沥青相和脱沥青油在溶剂中的溶液。 然后将溶剂与脱沥青油分离,通过将溶液切向地穿过孔半径的无机膜从2至15个非计算机:所得滤液具有增加的溶剂含量并可循环使用。 脱沥青油选择性地保留在膜的上游侧。

    Intensive hydrofining of petroleum fractions
    2.
    发明授权
    Intensive hydrofining of petroleum fractions 失效
    石油馏分的加氢精制

    公开(公告)号:US5954950A

    公开(公告)日:1999-09-21

    申请号:US524631

    申请日:1995-09-07

    IPC分类号: C10G49/00 C10G25/00

    CPC分类号: C10G49/002

    摘要: Intensive hydrofining of petroleum fractions wherein an at least partly together with hydrogen circulate in a given direction, in at least one reactor containing at least one fixed bed of a hydrofining catalyst in solid form, is characterized in that the reactor is equipped with at least one inlet pipe for the mixture of the petroleum fraction and hydrogen and at least one outlet pipe for the resultant hydrofined petroleum fraction, and that at least one static mixer is positioned upstream from said outlet of the hydrofined petroleum fraction.

    摘要翻译: 石油馏分的强化加氢精制,其中至少部分与氢在给定方向循环,在至少一个含有至少一个固体床形式的加氢精制催化剂固定床的反应器中,其特征在于反应器配备有至少一种 用于石油馏分和氢气的混合物的入口管和用于所得加氢精制石油馏分的至少一个出口管,并且至少一个静态混合器位于加氢精炼馏分的出口的上游。

    Selective hydrogenation of hydrocarbon cuts containing monounsaturated
and polyunsaturated hydrocarbons
    3.
    发明授权
    Selective hydrogenation of hydrocarbon cuts containing monounsaturated and polyunsaturated hydrocarbons 失效
    含有单不饱和烃和多不饱和烃的烃馏分的选择氢化

    公开(公告)号:US5817901A

    公开(公告)日:1998-10-06

    申请号:US524573

    申请日:1995-09-07

    CPC分类号: C07C7/167 C10G70/02

    摘要: A process for the selective hydrogenation of a fraction of hydrocarbons containing 2 to 20 carbon atoms and comprising monounsaturated olefinic hydrocarbons and/or aromatic compounds and at least one polyunsaturated hydrocarbon from the group formed by acetylenic compounds and dienes, in which the hydrocarbon fraction, which is at least partially in the liquid phase, circulates with hydrogen in a given direction in a reactor containing at least one fixed bed of a hydrogenation catalyst in the form of a divided solid, characterized in that said reactor is provided with at least one inlet conduit for a fluid mixture comprising said hydrocarbon fraction and hydrogen and at least one outlet conduit for the hydrogenated hydrocarbon fraction, and in that it comprises at least one static mixer upstream of said outlet for the hydrogenated hydrocarbon fraction.

    摘要翻译: 一种含有2至20个碳原子的烃馏分的选择性氢化的方法,包括单不饱和烯烃和/或芳族化合物和至少一种由炔属化合物和二烯形成的基团中的多不饱和烃,其中烃馏分 至少部分地在液相中,在含有至少一种分解固体形式的氢化催化剂的固定床的反应器中,以给定方向在氢气中循环,其特征在于,所述反应器设置有至少一个入口导管 用于包含所述烃馏分和氢气的流体混合物和用于氢化烃馏分的至少一个出口导管,并且其包含在所述加氢烃馏分出口上游的至少一个静态混合器。